Process to maintain large clean recreational water bodies

ABSTRACT

The invention discloses a process to implement and maintain large water bodies with color, transparency, and cleanness characteristics similar to swimming pools or tropical seas, at low cost. The present invention also discloses a structure to contain large water bodies, comprising a system for the removal of impurities and surface oils by means of skimmers and a suction device to clean said structure.

This application is a Continuation of U.S. Ser. No. 12/884,872, filed 17 Jun. 2010, which is a Continuation of U.S. Ser. No. 11/819,017, filed 25 Jun. 2007, now U.S. Pat. No. 7,820,055, which claims benefit of Serial No. 3225-2006, filed 21 Nov. 2006 in Chile and which applications are incorporated herein by reference. To the extent appropriate, a claim of priority is made to each of the above disclosed applications.

FIELD OF THE INVENTION

This invention discloses a process to obtain (i.e., to implement and maintain) large water bodies or volumes for recreational use, such as lakes or ponds with excellent color, high transparency and cleanness characteristics similar to swimming pools or tropical seas at low cost, in particular for water bodies larger than 15,000 m³. The invention also comprises a device to extract a particulate material decanted from the water by using the aforementioned process. Furthermore, the present invention discloses a structure to contain large water bodies or volumes, which is specially designed to carry out said process. The decantation process together with the device to extract a decanted material from the water, plus the arrangement of the large volume structure with its functional characteristics of water surface displacement, allow replacing traditional filtration as used in conventional swimming pools that would be very onerous and inefficient in systems having large bodies or volumes.

BACKGROUND OF THE INVENTION

When a nutrient enters into water, aerobic organisms consume dissolved oxygen as a result of the induced metabolic activity. Thus, the nutrient exerts a demand on dissolved oxygen availability, which is called biological oxygen demand (BOD). If the amount of organic material in the medium is very high, it can lead to a decrease in dissolved oxygen concentration. At low oxygen levels, aquatic environment promote the growth of anaerobic species.

Anaerobic metabolism is much slower than aerobic processes (typically more than one order of magnitude) have lower efficiency, and generates various intermediate organic compounds (e.g. organic acids, alcohols, methane). As a result of the lower rate of dissolved organic matter consumption, this will accumulate in the aquatic environment.

If dissolved oxygen is consumed faster than it can be replenished, water starts to deoxygenate. No strictly aerobic organism, from microorganisms to fish, will survive in said water. Thus, organic contaminants will accumulate and further establish anaerobic conditions, which generate malodorous substances (e.g. sulfides and volatile amines) and partially oxidized organic compounds.

In addition to bad smell, anaerobic conditions can raise human health issues, because many anaerobic bacteria are pathogenic (for instance, tetanus, and botulism). When the water contains dissolved sulfates, reducing anaerobic bacteria produce H₂S (corrosive and poisonous).

The increase of the amount of nutrients required for life in a water body is called eutrophication. Eutrophication is defined as the process of nutrient enrichment in a water body. It is a natural phenomenon in the ageing process of ponds and lakes (eutrophic lakes). On the contrary, a young water body, poor in nutrients required for life, is called oligotrophic. The nutrient increase in the pond promotes a higher production of aquatic plants and animals. Said organic matter increase generates in its turn an increase of the organic content of sediments. Eutrophication can generate serious problems in superficial water bodies.

Photosynthesis implies the creation of organic matter from inorganic materials and therefore the production of large amounts of organic substances where there were only little amounts before. When algae/plants die, their components are transformed in organic nutrients that exert an oxygen demand.

During photosynthetic action, CO₂ is readily consumed, thus producing a rise in pH, which can attain a value over 10. During the night, the inverse reaction occurs, consuming oxygen and generating CO₂, with which pH tends to drop. Photosynthetic activity has a significant effect on the pH level of the water body, because it affects the reversible reaction. HCO³⁻+H+←—→CO₂+H₂O

Finally, the masses of algae deposited in the shore die and rotten, thus producing anaerobic conditions, which present health dangers (e.g. formation of Clostridium botulinum, a strictly anaerobic pathogen microorganism). On the other hand, aquatic plant ramifications retain organic solids that decompose, which exerts a concentrated oxygen demand.

Generally, nitrogen N and phosphorus P are the limiting factors. In microorganism growth, P is consumed as phosphate, while the major part of bacteria assimilate N under the form of NH₃, and only some of them assimilate N as NO₃ ⁻. Inversely, algae assimilate N as NO₃ ⁻ and very few use NH₃. There are more bacteria able to use NO₃ ⁻ as oxygen source than as N source. According to the approximate stoichiometry of photosynthesis in algae, N:P ratio is in the order of 7:1. According to the Liebig minimum law, an N:P ratio much higher than 7 in a water body indicates that P is the limiting nutrient; on the other hand, an N:P ratio value much lower than 7 implies an N limitation. Some authors suggest that P and N concentrations higher than 0.015 and 0.3 mg/l, respectively, are enough to generate an excessive growth of algae in lake waters.

The main sources of organic N are proteins, amino acids and urea; on the other side, inorganic N is in the form of NH₃, NO₃ ⁻, NO₂ ⁻. Ammonia is a characteristic product of organic matter decomposition, and it can be microbiologically oxidized to nitrites and nitrates by the action of nitrifying bacteria. These processes occur naturally in water and constitute a major contribution to the biological oxygen demand.

When artificial water bodies are formed, such as lakes or ponds, water quality deteriorates progressively. Depending on the nutrient contribution, it can be reached any state from equilibrium in which algae, aquatic plants, bacteria, insects and fish survive in stable condition to eutrophication processes in which the excessive contribution of nutrients produces a high proliferation of algae and aquatic plants. When these die, they are decomposed by bacteria in aerobic processes that consume the oxygen. When oxygen decreases, many organic remainders remain deposited in the bottom, thus increasing sediments and suffering processes that increase turbidity, bad smells are produced and the physicochemical and sanitary quality of the water is impaired, which reduces the possibilities of recreational use.

To mitigate these effects different techniques are used, such as aeration systems to increase oxygen levels, algaecides and herbicides to control the excessive proliferation of algae and aquatic plants, the use of biological filters to decrease nutrient contribution, fish and zooplancton to reduce algae, nutrient capture by means of chemicals, inoculation of bacteria to digest organic matter, colorants to improve the aesthetic appearance, mechanic removal of algae and aquatic plants, the use of dredges to decrease the amount of sediment, clarifying agents to decrease turbidity, etc.

The characteristics and quality of the water of these ponds are very different to those of swimming pools. In the first case, an ecological equilibrium between different species must be attained, while in the second case the objective is the removal of organisms and impurities. Therefore, very different turbidity, color and physicochemical characteristics standards are accepted.

To keep swimming pool water transparent and apt for bathing, filtration systems are used, mainly sand, diatomaceous earth and cartridge filtration systems. The entire water must be filtered every 4 to 12 hours, depending on the type of swimming pool.

In addition, organic matter oxidants, disinfectants, algaecides and eventually pH regulators and clarifiers must be used to keep aesthetic and sanitary conditions. Depending on each country's regulation, swimming pools are required to keep minimal disinfectant residual concentrations or permanent redox potential (ORP) levels between 650 mV and 750 mV.

The application of the swimming pool technology to large water bodies to obtain optimal water quality is not possible due to the high cost of the installations and the involved operative costs.

To illustrate this situation, we can recall that if the water body to be filtered is the one described below in the application example of 250,000 m³, complying with the minimal regulations of Chilean Swimming Pools (T=2 en NCh 209, example country for the application), 2,983 liters per second are required to be filtered, which corresponds to the water volume treated by a potable water plant for a city. An Olympic swimming pool has 2,500 m³ (50×25×2 m), which corresponds to 1% of the considered volume in the application example of this patent application.

The same is true when swimming pools chemicals are to be applied to these volumes. The water volume of the application example of this invention corresponds to 4,000 10-meters-long swimming pools.

The control of disinfectants in swimming pools and spas by means of the measurement of the (ORP) has been used for many years with good results. ROP measures the oxidizing power of the disinfectant or, in other words, its real concentration-independent chemical activity. Direct measurement of disinfectant concentration can lead to error, because the activity can be decreased depending on pH and the presence of contaminants, even at high concentrations. In fact, studies have demonstrated that bacterial life in water is more dependent on ROP than on oxidant concentration. To remove undesired microorganisms in swimming pools, normally a ROP value between 650 mV and 750 mV is permanently maintained (public swimming pool regulations in developed countries require more than 700 mV permanently) at a normal pH between 7.2 and 7.6. This is not possible with large water bodies due to the high implied costs.

The previously exposed facts make maintaining large water bodies (over 15,000 m³) using filtration and disinfection technologies similar to those of swimming pools for recreational use largely unviable.

Therefore, there are no large artificial ponds or dams with the aesthetic and sanitary characteristics of swimming pools or tropical seas that have clarity levels higher than 25 and even 40 meters.

The technical problem solved with the present invention is the achievement of these characteristics in large water bodies at low cost.

STATE OF THE ART

Invention patents protecting treatment processes for large volumes of water such as ponds and dams were found at world level. In what follows, an analysis of the most relevant documents and their relation with the technology to be protected is performed.

Invention patent applications JP4115008 and JP7310311 protect artificial ponds connected to the sea that have as objective the purification of sea water. The system allows the entrance of water to the pond, where it follows a path specially designed to remove contaminants or it is conducted to a purification facility to be subsequently returned to the sea. Clearly, the Japanese invention has no relation with the type of pond that is desired to protect in this application.

The invention patent application FR2740493 protects a pool or artificial lake constructed with a flexible bottom comprising a textile net and concrete. The invention includes a draining system and injectors around the border that allow the diffusion of a liquid to the draining system. The analyzed invention does not have relation with the artificial pond or the process that is to be protected.

The invention patent application JP59222294 protects a purification process for river and lake water to remove N, P, BOD (biological oxygen demand), etc. that implies pumping the water through a bed filled with certain mineral. The Japanese invention allows cleaning pond water, but based on water pumping through a packed bed, which is equivalent to filtering the liquid. Therefore, the Japanese invention does not have relation with the technology that is to be protected.

The invention patent application CN1256250 protects a water purification process that includes microflocculation with an inorganic flocculant with high molecular weight and direct deep bed filtration. The analyzed process corresponds to an assisted flocculation with faster and more efficient results, but in no case it affects the novelty or the inventive level of the process of the present invention.

From the analysis of the former documents, it is possible to conclude that there are no processes or artificial ponds similar to those to be protected, which allow obtaining water bodies larger than 15,000 m³ for recreational use, with color, transparency and cleanness characteristics similar to swimming pools or tropical seas at low cost, because in the process of the present invention the traditional filtration step has been substituted by a suspended-solid flocculation step and subsequent cleaning with a suction device, designed for said function, together with the generation of a displacement of surface water that contains impurities and surface oils by means of injecting inlet water and evacuating said water through skimmers (surface slots and dumps) comprised in the structure, and disinfection has been achieved by the application of controlled oxidation pulses.

The present invention is related to a process to obtain large water bodies or volumes (wherein the term obtaining is meant to be understood as implementation and maintenance), wherein a structure is provided (having elements required for water treatment and features that produce the desired results) to contain the water, and separation and flocculation (maintenance) processes of particles that make water cloudy and impure are performed, in such a way that flocculated material is suctioned by a suction device once flocculation has taken place, and oily materials are removed through skimmers (surface slots or dumps) of the structure of the present invention, said structure having pipes that feed fresh water to fulfill the desired objective.

DESCRIPTION OF THE FIGURES

Brief description of the figures.

FIG. 1 shows a side view of the suction device.

FIG. 2 shows a top view of the structure of the suction device.

FIG. 3 a shows a front view of the structure of the suction device.

FIG. 3 b shows a front view of the structure of the suction device.

FIG. 4 a shows a right side view of the suction device.

FIG. 4 b shows a left side view of the suction device.

FIG. 4 c shows a rear view of the suction device.

FIG. 5 a shows a top view of the structure of the suction device.

FIG. 5 b shows a top view of the suction device.

FIG. 6 shows a schematic view of the cleaning system with the suction device.

FIG. 7 shows a detailed schematic view of the suction system with the suction device.

FIG. 8 shows a schematic view of the suction device.

FIG. 9 shows a schematic view of the structure of the suction device;

FIG. 10 shows a top view of the structure of the water body of the present invention.

DETAILED DESCRIPTION OF THE FIGURES

FIG. 1 shows the following components: moving direction (2) of the suction device, PVC pipe for suction connection (8), bottom opening (14) in PVC pipe (27) for bottom suction, sanitary T pipe (9), steel frame (10), auto-lubricated plastic wheels (12), supporting plate (19 a) for the axles of the wheels and rollers (19 b), plastic-based brushes with synthetic bristles made of polyethylene or the like (20), steel platen with perforations or slots (21) to fasten the brushes (20) in a continuous line.

FIG. 2 shows the moving direction (2); the frame (10) to which supporting plates (19 a) are affixed to support wheels and rollers axles (19 b) for high density polyurethane rollers (11) that are intercalated with wheels (12), which are lined up and also supported by supporting plates (19 a); a brush line (16) fastened to the perforated platen (21) provided with the structure; and the suction line (27) can be observed in the central zone of the device, formed by a PVC tube with five rectangular bottom openings on wall (14), closed in both ends with a cap made of the same material (17).

In FIGS. 3 a and 3 b the device structure is shown, wherein a supporting plate (1) can be observed for the pulling tensors welded to the frame (10), a resin cover reinforced with fiberglass over a galvanized iron network (6), a lateral plastic membrane flap (7), rollers (11), wheels (12) and sanitary PVC pipes (8) having sanitary T pipes (9) at their bottom section, and a PVC suction pipe or line (27) attached to the open endings of said T pipes, said suction pipe or line (27) having openings wherein the opening area will be proportional to the installed suction capacity.

FIG. 4 a shows a lateral right view of the device with the moving direction (2), a supporting plate (1) for the pulling tensors, whereas from the center a PVC suction pipe (8) emerges having a resin fiber collar attached at its base, said resin fiber collar being formed with fiberglass reinforcements (4) for the fastening and sealing of suction tubes, handles (5) for pulling, handling and lifting the device, the resin cover (6) and the lateral membrane flap (7). FIG. 4 b shows a left side view of the device indicating the moving direction (2) and the device cover (6). FIG. 4 c shows a rear view of the device indicating the device cover (6).

FIG. 5 a shows a top view of the device structure indicating the moving direction (2) and FIG. 5 b shows a top view of the device indicating the moving direction (2).

FIG. 6 shows the cleaning system with the suction device placed in the water body (41), wherein there is a pipe to draining chamber (28), plastic buoys (29) for floating a hose (36), platform (30) for the steersman and the deck operator of the boat (31) for pulling with an incorporated four-stroke engine and protected propeller, a pulling tubular labeled galvanized-steel connecting rod (32) astern, a suction device (33), a connection hose (34) from the boat (31) to the device (33), a connection piece (35) of the connection hose (34) with the suction hose (36), and a suction hose (36) that connects the movable electric suction pump (37) at the lake's shore with the boat (31).

FIG. 7 shows a longitudinal section of the suction device in which the partial configuration of the structural frame (10), the pulling rod (32) that connects the device (33) (not shown in this figure) to the pulling boat, the set of symmetric suction pieces (38) that connect the suction pipes (27) of the cart with the hose (34) connecting the device to the boat is described. In this figure also appear the projections of wheels (12) and rollers (11).

FIG. 8 shows a lateral view of the pulling boat (31), the suction device (33) placed in the bottom of the water body (41) of the lake, the placement of the roofed platform (30) for the boat operator, the connecting rods (32) between the device (33) and the boat (31), the symmetrical suction elements (38), and the connecting hose (34) with coupling pipe in the boat (35).

In FIG. 9, a rear view of the system is shown, indicating the connection hose (34), the pulling rods (32), the set of coupling pieces (38) for symmetrical suction from all four device inlets toward the connecting hose (34), the hose (36) with floats (29) that connects the boat connector (35) with the suction pump on land (37), and the pipe that leads to the drainage (28).

In FIG. 10, the following elements of the structure can be observed: recycle pipe (39) onto which injectors are arranged; injectors (40) arranged along all the perimeter of the water body; water body (41) contained by the structure; skimmers (42) for removal of floating contaminants such as water with oils; water inlet line and chamber (43) where water is extracted to feed the lagoon; zone of restricted natural circulation (44); fresh water feeding point (45) to the lagoon.

DESCRIPTION OF THE INVENTION

This invention comprises a process to obtain (i.e., to implement and maintain) large water bodies or volumes for recreational use with excellent color, high transparency and cleanness characteristics similar to swimming pools or tropical seas at low cost, in particular for water bodies larger than 15,000 m³, such as artificial ponds or dams for recreational use. The present invention also discloses a structure to contain large water volumes. The invention also comprises a suction cart or suction device to extract a particulate material decanted from the water. The process of the present invention comprises in a first step providing a structure to contain large water volumes such as artificial lakes or ponds, with elements that allow water treatment and features required to obtain the desired aesthetic and sanitary results of having “color, transparency and cleanness similar to swimming pools or tropical seas at low cost”.

The process has a great advantage over the previous art in that the desired characteristics are achieved without needing a filtration system or adding large amounts of chemicals, which opens the possibility to implement and maintain large crystalline water bodies with no size limit.

The process of the invention comprises the following steps or stages:

a.—providing a structure with skimmers able to contain a large water body larger than 15,000 m³.

b.—feeding the structure of step (a) with inlet water having iron and manganese levels lower than 1.5 ppm and turbidity lower than 5 NTU.

c.—measuring water pH, ideally it should be within a range lower than 7.8;

d.—adding an oxidizing agent to the water contained in the structure of step (a), with which a 600 mV minimal ROP is controlled in water for a minimal period of 4 hours and in maximal cycles of 48 hours;

e.—adding a flocculating agent in concentrations within 0.02 and 1 ppm with maximal frequencies of 6 days and cleaning the bottom of the structure of step (a) with a suction device to remove precipitated impurities from the bottom of said structure, together with the additional flocculants and;

f.—generating a displacement of surface water containing impurities and surface oils by means of the injection of inlet water according to step (b), which generates said displacement in such a way to remove said surface water by means of a system for impurities and surface oils removal arranged in the structure of step (a).

It is worth mentioning that cleaning is performed in such a way that every sector of the structure is cleaned in time intervals no greater than 7 days, in such a way as to replace the traditional filtering performed in conventional size structures.

In the disclosed structure or lake in step (a) it should be maintained a minimal total water renewal rate of 150 days, preferably 60 days, to avoid the accumulation of oxidation products (ageing).

Each step of the process to implement and maintain large water bodies is separately detailed below, in the understanding that every obvious change will be encompassed within the scope of the present invention.

In step (a), a structure or pond is provided to contain a large water body larger that 15,000 m³, with elements that allow water treatment and features required to obtain the desired aesthetic and sanitary results of having “color, transparency and cleanness similar to swimming pools or tropical seas at low cost”. The features of the structure provided to carry out steps (b) to (f) of the invention will be noted by the reader when the structure specially designed for this invention is specifically described.

In step (b), and only in the case where it should be required, a water pre-filtering and treatment can be carried out on the water that is incorporated into the lake, in the case wherein the water contains incrusting micro-mollusks or turbidity levels over 5 NTU. Nevertheless, water inlet should not include micro-mollusks and metals such as iron or magnesium in order to maintain the aforementioned ranges. In other words, low turbidity water is preferable because the process of the present invention does not have a traditional filtration process and the suction device and skimmers would be inefficient in case of receiving high levels of suspended particles, including both organic and inorganic contaminants.

If in step (c) the pH is higher than 7.8, it is necessary to add bromine salts such as sodium bromide, always keeping minimal bromide concentrations of 0.6 ppm. It is worth mentioning that in the case of sea water, in spite of having pH values higher that 7.8, it naturally contains high bromide levels, and therefore it is not necessary to add this element if the artificial pond or lake is filled with sea water.

In step (d), to maintain a minimal redox potential of 600 mV in the water for a minimal period of 4 hours in maximal cycles of 48 hours, preferably 24 hours, oxidant agents are added such as: ozone, sodium or potassium persulfate, chlorine derivatives, hydrogen peroxide, bromine derivatives or by electrochlorination. The amount of applied oxidant is controlled by permanent measurement of ROP during the application in such a way that it fulfills the minimal established requirements, i.e. oxidant is added up to achieve a minimal of 600 mV during a period of 4 hours.

The type of oxidant depends on the cost, among other factors. Hypochlorite produced by electrochlorination and ozone are economical because they are produced in situ, but require high equipment investments.

The applied amount depends on many factors that vary daily, such as, for instance: temperature, solar radiation, environmental contamination, rain, storms, levels of use, etc. In short, the necessary oxidant amount is determined by ROP measurement.

Notwithstanding the foregoing and without limiting the invention, it can be stated that the usually used concentrations and the oxidant application ranges are those indicated in Table 1:

TABLE 1 Oxidant Application USUAL OXIDANT CONCENTRATION * MIN-MAX RANGE Ozone 0.05 ppm 0.01-0.58 ppm Hydrogen peroxide 0.04 ppm 0.01-0.46 ppm Sodium hypochlorite 0.16 ppm 0.04-1.50 ppm Persulfate 0.28 ppm 0.07-3.30 ppm Bromines 0.22 ppm 0.05-1.80 ppm * Total amount added to reach and maintain the minimal 600 mV ROP for 4 hours, divided by the total volume of the water body.

Step (e) includes adding a flocculating agent and cleaning the bottom of the structure of step (a) with a suction device in order to remove precipitated impurities from the bottom of the lake, together with the flocculant agents.

Cleaning is performed in such a way that every sector of the lake is cleaned in time intervals no greater than 7 days, preferably every 4 days. With this step, together with the use of skimmers, traditional filtering processes used in swimming pools are replaced.

Among flocculants that can be added in this step (e), a cationic polymer is preferred, e.g. HICAT-1™, which is a biodegradable cationic polyelectrolyte with 25% solids, produced by Buckman Laboratories in the United States (it is accepted by the National Health Service of Chile and recommended to be used in swimming pools at concentrations 100 times higher) in concentrations between 0.02 and 1 ppm with maximal frequencies of 6 days, preferably 0.05 ppm every 24 hours; or addition of Crystal Clear™, which is a biodegradable cationic polyelectrolyte produced by AP Aquarium Products in the United States (it is used in aquariums in concentrations 100 times higher) in concentrations between 0.04 and 2 ppm with maximal frequencies of 4 days, preferably 0.16 ppm every 24 hours.

Additionally, this step can include adding algaecides such as quaternary ammoniums (e.g. polyquats) and/or copper compounds (e.g. CuSO₄·5 H₂O or copper chelates), keeping copper levels between 1 ppb and 1.5 ppm, depending on temperature and sunlight; 0.3 to 1.5 ppm of copper for temperature ranges between 10° C. and 30° C.

It is important to keep in mind that the objective of the suction device is not only the cleaning of the bottom in the described process, as is the case of vacuum devices of traditional pools, but that said suction device replaces completely the traditional filtering system of swimming pools together with the use of flocculants. Furthermore, the fact that the process contemplates the displacement and removal of superficial water with impurities toward the structure slots complements the action of the suction device.

In other words, the suction device not only removes material naturally deposited on the bottom (leaves, branches, earth, etc.) but also all the suspended particles that are eliminated by filtration in the case of swimming pools and that are converted into floccules (large particles) and are suctioned by the device in this invention, thus decreasing their removal costs in two orders of magnitude.

In step (f) it is necessary to control the levels of injection of fresh water to ensure the correct displacement and removal of superficial water with impurities and oils through the skimmers of the structure provided in step (a) of the process of the invention.

As hereinabove mentioned, to carry out the process to implement and maintain large bodies of water larger that 15,000 m³ according to the present invention, it is necessary to provide a structure like that shown as an example in FIG. 10.

The structure or pond according to the present invention includes bottoms and walls built with low permeability materials such as clay and bentonite, coated by a non-porous material, such as a polyvinyl chloride membrane, lineal low density polyethylene or high density polyethylene capable of being cleaned, with a depth of at least 0.5 meters, a system for removing impurities and superficial oils by means of skimmers, a feeding pipe system that allows water replacement by entrance of fresh water, a feed water intake system, which can be marine water, well water, spring water or water from other sources; in the case of marine water the intake system can be through headers or wells positioned at a depth of more than 6 meters.

The relevance of the structure to solve the technical problem proposed in the process of the present invention is detailed as follows:

The structure must have skimmers to remove surface oils and particles, since otherwise they accumulate and deter water quality, even after performing all the chemical treatment steps, since these do not remove floating greases or solids. In this way, the final objective of obtaining “color, transparency and cleanness characteristics similar to swimming pools or tropical seas at low cost” would not be fulfilled without these skimmers. The process of movement of superficial water toward the skimmers caused by fresh water entry together with the flocculant-suction device system replaces the traditional filtering system of swimming pools.

The structure must have fresh water feeding pipes that allow causing the surface water movement that eliminates floating impurities and oils through the skimmers. These pipes contribute also the fresh water necessary to refresh water at the described rates, since otherwise oxidation sub-products accumulate, which render chemical treatments inefficient and deter water quality, not fulfilling the “color, transparency and cleanness characteristics similar to swimming pools or tropical seas at low cost”.

The structure has a pipe network with injectors that allow an efficient application of the products and water homogenization. In swimming pools this is irrelevant, but in large volume water bodies the existence of isolated stagnant zones creates contamination centers that make disinfection treatments inefficient, thus deterring water quality and not fulfilling the fundamental objective of obtaining “color, transparency and cleanness characteristics similar to swimming pools or tropical seas at low cost”.

The plastic liner must have special non-porous characteristics. In swimming pools this may be irrelevant, but in large volume water bodies cleaning would be unfeasible with adherent linings and a dark layer would form that do not allow obtaining the desired result, namely “color, transparency and cleanness characteristics similar to swimming pools or tropical seas at low cost”.

The bottoms and walls must be built with low-permeability materials such as clay and bentonite, lined with a non-porous material such as polyvinyl chloride membrane, etc. This is the economic way of constructing these large water bodies, since if known building techniques for swimming pools or ponds would be used, the objective of “low cost” would not be obtained.

Water intake must be done in such a way as to avoid micro-mollusks, since besides blocking recycle pipes, said micro-mollusks adhere to surfaces generating a dark color that prevents obtaining the objective of “color, transparency and cleanness characteristics similar to swimming pools or tropical seas at low cost”.

Water intake must avoid water with metals such as iron and manganese, since this pond does not have traditional filtration and the flocculation treatment and suction device are inefficient at removing inorganic impurities, including metallic contaminants.

The crystalline structures or ponds must have water intakes that allow using low cost water since, in contrast to swimming pools that recycle water through their filters, in this case the water from the skimmers and the suction cart or device is disposed of.

The structure provided in step (a) for the process of the invention has additionally:

1) light blue, white or light yellow bottom (liner) color, for the water to take the color of tropical seas, i.e. “color, transparency and cleanness characteristics similar to swimming pools or tropical seas at low cost”. This is obvious in the case of swimming pools, but large ponds use dark plastics due to their durability and lower cost; that is the reason why there are no large water bodies with the described colors. For instance, if the plastic would be black (usual in ponds), the desired color would not be obtained even if the water had high quality and transparency.

2) a depth over 0.5 meters, preferably between 2 and 5 meters; Depth is important to achieve the desired color “similar to tropical seas”, since if it is too shallow the water does not reach turquoise shades of color and resembles a light-colored water body. Moreover, due to the high water transparency of these ponds, if depth is too low UV light penetration deters the liner rapidly, thus not obtaining the desired low cost.

3) a recycling system by means of pipes with injectors that allow maintaining water homogeneity and avoiding stagnating zones. This system can be avoided in windy zones.

4) the structure must be constructed in such a way that it avoids dragging organic matter such as leaves and soil by effect of wind, watering, etc.

5) Optionally, it can be made of cement with coatings such as painting, poliurethanes or fiberglass.

Therefore, the structure is fundamental for the process of the invention, since in said structure it is also possible to generate a step consisting of the displacement of surface water containing impurities and oils by means of a current generated by fresh water injection through the pipe systems of said structure, thus removing said impurities and oils through said skimmers.

In the following, the suction device of the present invention is described in detail:

The suction device to carry out the cleaning of the structure bottoms, which is performed in step (e) of the process of the invention, comprises: a supporting plate, a resin collar reinforced with fiberglass, pulling handles, a resin cover, a lateral membrane flap, a steel frame, high density polyurethane rollers, auto-lubricated plastic wheels, an opening in a PVC pipe to suction the bottom, a brush line comprising plastic-based brushes with synthetic bristles and a steel platen with perforations or slots to fasten the brushes in a continuous line, supporting plates for the axles of the wheels and the rollers, and a suction PVC line with openings (see description of figures for more details).

The suction device operates by suctioning dirt through connecting hoses by means of a pumping system, said device being pulled by a system that includes a propelling device to move the suction device, such as a boat, for instance, a draining chamber, plastic buoys for aiding a hose to float, a platform for the steersman and the boat's deck operator in case a boat is used as propelling device, a pulling tubular labeled galvanized-steel connecting rod astern, a connection hose between the boat and the cart, a connection piece between the connecting hose and the suction hose that connects the pump placed at the structure edge. In any case, the propelling device of the suction device can also be formed by a remote mechanical traction system arranged out of the structure or any other propelling device useful to move the suction device.

The suction device is mainly formed by a structuring frame, a covering carcass with coupling means to be coupled to the pumping system, rolling means for continuous displacement over the surface to be cleaned and cleaning means consisting of a suction line and a brush line to remove the material to be cleaned by means of suction from the pumping system through the suction device.

The covering carcass comprises a laminar resin body that covers the structuring frame and the rolling and suction means. From the top section of the covering carcass supporting plates emerge for the pulling tensors from the boat, which are internally joined to the structuring frame; at its top section, said carcass also has suction PVC tubes that form coupling means to the pumping system and are attached by their base section to a carcass collar formed in molded resin fiber with glass fiber reinforcements for supporting and sealing said suction tubes; whereas from said carcass collar a resin mantle and a lateral membrane flap project to form the carcass body. Also its top section has handles for pulling, handling and raising the device.

The structuring frame is a steel frame to which an aligned series of steel plates for supporting the rolling means, which comprise the axles of high density polyurethane rollers and plastic auto-lubricated wheels, is supportively joined, and a perforated or slotted steel platen is likewise attached to support by means of bolts a continuous line of brushes having a plastic base and synthetic polyethylene bristles, or the like, which help in the task of removing the material to be suctioned. To the rear section, the abovementioned supporting plates of the pulling tensors are joined.

The cleaning means comprise a suction line formed by vertical PVC tubes, corresponding to suction tubes emerging upwardly from the covering carcass, to which T-shaped PVC tubes are attached at their bottom part, which are coupled in turn to horizontal tubes that have suction openings in their bottom part through which the removed material enters to be suctioned and taken out of the pond.

It is important to keep in mind that the objective of the suction device (suction cart) is not only the cleaning of the bottom in the described process, as is the case of vacuum devices of swimming pools, but that said suction device replaces completely the traditional filtering system of swimming pools together with the use of flocculants and the skimmer system.

If all the abovementioned elements are not present, water impurities accumulate and deter water quality, and so the final objective of the present invention, i.e. obtaining water bodies with “color, transparency and cleanness characteristics similar to swimming pools or tropical seas” at low cost, would not be obtained.

APPLICATION EXAMPLE

To carry out the process of the invention to implement and maintain water bodies larger than 15,000 m³ for recreational use with color, transparency and cleanness characteristics similar to swimming pools or tropical seas at low cost, the following steps or stages were performed:

A structure similar to an artificial lagoon was built in the central Chilean shore, having a length of 1 kilometer, an area of 80,000 m² and a volume of 250,000 m³ (33″20′59.91″S; 71″39′10.10″W). The bottom was built using clay and bentonite, and it was lined with lineal low density polyethylene (LLDPE) and high density polyethylene (HDPE) plastic with white and yellow color. The walls were built in cement and clay and lined with LLDPE and HDPE membranes.

Minimal and maximal depths were 1.2 and 3.5 meters, being 2.8 meters the average depth.

A pipe system of 100 to 250 mm diameter was installed all around the lagoon borders to facilitate recycling. The system has homogeneously distributed injectors every 10 meters around the entire lagoon that are placed in the bottom to inject the products and maintain water homogeneity. Systems for the removal of impurities and superficial oils by skimmers were installed.

Water intake for this structure was achieved through headers. Inlet water had 0.08 ppm iron and 0.15 ppm manganese, and a turbidity of 1.4 NTU. The water had a pH of 7.93 and natural bromine concentrations of 48 ppm, and consequently no addition of bromine salts was required. The water was impounded through headers at a depth of 8 m at sea shore. The intake was performed at this depth to avoid incrusting micro-mollusks. The presence of micro-mollusks in sea water causes problems by growing, development and adhesion to piping walls and lagoon structures. Other possible way to avoid incrusting micro-mollusks is the use of water pre-filtering.

ROP value was maintained over 600 millivolts (mV) during 4 hours in 24-hour cycles. This was achieved by applying oxidants, such as e.g. ozone, hydrogen peroxide, potassium persulfate, electrochlorination or sodium hypochlorite. All the former were tested with good results.

In an average September day with an air temperature between 10 and 16° C. and a water temperature of 17° C., 0.11 ppm of sodium hypochlorite produced by electrochlorination were applied, which was sufficient to maintain ROP over 600 mV for more than 4 hours. This system is advantageous when working with salt water, because the electrolytic process transforms chloride in sea water in hypochlorite, with no need to add additional chemicals.

The established regulations for swimming pools in other countries indicate higher ROP values (between 650 and 750 mV) permanently, but this is not economically viable in large volumes of water and in this invention it has been demonstrated that keeping ROP over 600 mV during 4 hours in 24-hour cycles is enough to decrease the growth of microalgae and microorganisms in large water bodies, thus generating low-contamination conditions apt for swimming.

The bacteria Escherichia coli, a bacterial pathogen marker, dies after 100 seconds when exposed to a ROP of 600 mV, and consequently the 4-hour treatments have a high disinfectant power.

The water body volume of this example equals the volume of 6,000 familiar 8-meters-long swimming pools and is constructed in such a way that it does not receive visible contamination from the surroundings (leaves, soil, watercourses), and consequently contamination received from the environment is very low in relative terms when compared with a swimming pool. Proportionally, human contamination is also insignificant given the high dilution power (for example, 4 swimmers in a familiar pool equal 24,000 swimmers in the lagoon).

Additionally, the flocculation and bottom cleaning with the suction cart, and the removal of grease and superficial impurities by means of the skimmers allows keeping low organic matter levels, which decreases the use of oxidants.

Algaecide action was achieved by keeping an average copper level in the water of around 0.3 ppm, and the application was made by using copper salts (copper sulfate pentahydrate) in closed sacs, which is applied in the chambers through which recycling system water passes, in such a way that the salts dissolve slowly, and also by an copper electrode ionization process in which an electric current is applied to said electrodes and copper ions are released into the medium in a controlled way. Measured copper levels varied between 0.1 ppm at a temperature of 10° C. and 1.5 ppm at 30° C. (2 ppm are acceptable in potable water, see Table 4).

A cationic flocculating polymer was added. The flocculant used was HICAT-1™ in daily applications of 0.04 ppm through the recycling system.

With the aid of the suction cart or device, the plastic of the bottom of the lagoon was cleaned subsequently to decantation. The device has a system of suction chambers, thus removing all the precipitated impurities together with the polymer, which allows the bottom of the lagoon (membrane) to be seen. The device that cleaned the plastic membrane was pulled by a boat and did not leave any residual layer, because it was a fine cleaning and not a dredging. This cleaning and suction method was permanent and the bottom of the lagoon was cleaned daily, in such a way that the suction system passes by every membrane sector every four days.

The water was maintained in movement by means of a recycling system that operated 8 hours per day in low-wind seasons, thus keeping water homogeneity. Injectors distributed around the structure throw the water up to a long distance and are placed every 10 meters. It should be mentioned that the water contained by the structure also shows an important circulation as an effect of the wind and it should be possible to decrease the artificial recirculation requirements by a suitable design of the structure, thus sparing energy.

This recycling system was used to apply chemicals. The water of the structure was completely renewed in a period between 30 and 150 days. The aim of the renewal was to avoid “water ageing”, which is the formation of secondary compounds derived from oxidation reactions. The renewal was performed by taking new water through the feeding pipes, independently from the recycling pipes that end at the injectors.

A superficial water outlet flow was kept by means of the skimmers that remove oils and superficial impurities.

The amount of added chemicals depends mainly on the temperature and is orders of magnitude lower than those required in swimming pools.

The total comparative maintenance cost per cubic meter was approximately 3% of the usual cost in swimming pools.

In this application example, the physicochemical conditions of water were determined to comply not only with regulations for recreational waters with direct contact (see Table 2), which are those applied in this case, but also with regulations for potable water (see Table 4), with the exception of characteristics inherent to sea water, and with regulations for swimming pools (see Table 3), with the exception of chlorine permanent residual levels, which do not apply because of the applied technology.

TABLE 2 Comparison of the water treated with the process of the invention and the regulation for recreational waters with direct contact (NCh 1333 *) MEASURED VALUE IN THE PARAMETERS LAGOON NCh 1333 pH 7.96 6.5 to 8.3 except if natural water conditions show different values, but in no case lower than 5.0 or higher than 9.0 Temperature, 17.7 30 ° C., maximal Clarity, minimal * 35 meters Visualization of Secchi discs at a depth of 1.20 meters Visible floating solids Absent Absent and unnatural foams Floating oils and <5  5 greases, mg/l, maximal * Emulsified oils and <5 10 greases, mg/l, maximal * Color, Pc-Co Scale unit, 10 100  maximal * Absent Absence of artificial colors Turbidity, Silica units, 0.55 50 maximal * Fecal coliforms/100 ml, <2.0 1,000   maximal * Substances that cause Absent Absent inconvenient smell or taste * Official Chilean regulations were used (Chile was the country of the application example), Chilean rule NCh 1333

TABLE 3 Comparison of the water treated with the process of the invention and the regulation for swimming pools (NCh 209 *) MEASURED VALUE PARAMETERS IN THE LAGOON NCh 209 pH 7.96 7.2-8.2 Free residual chlorine + 0.5-1.5 (ppm) Copper (algaecides) mg/l 0.38 1.5 maximal Bromine (disinfectant) mg/l + 1-3 Foam, grease and Absent Absent suspended particles Colonies of aerobic 2   ≦200 bacteria/ml Fecal coliforms Absent Absent Total coliforms ≦2    ≦20 colonies/100 ml Algae, larvae or other Absent Absent living organisms Clarity 35 meters 1.4 meters * Official Chilean regulations were used (Chile was the country of the application example), Chilean rule NCh 209 + Do not apply because of the applied technology

TABLE 4 Comparison of the water treated with the process of the invention and the regulation for potable water (NCh 409 *) MEASURED Official ASSAY VALUE IN THE 2005 NCh PARAMETERS UNIT METHOD LAGOON 409 pH — (I) 7.96 6.5 < pH < 8.5 Turbidity NTU (I) 0.55 2.0 True color at Pt—Co (I) 10    20   pH = 7.71 Smell — (I) Odorless Odorless Taste — (I) + Tasteless Ammonia mg/l NH₃ (I) 0.12 1.5 Total arsenic mg/l As (I) <0.005   0.01 ⁽¹⁾ Cadmium mg/l Cd (I) <0.002  0.01 Zinc mg/l Zn (I) <0.05  3.0 Total cyanide mg/l CN (I) <0.05   0.05 Chlorides mg/l Cl (I) 18,914     400 ⁽²⁾   Copper mg/l Cu (I) 0.38 2.0 Phenolic compounds mg/l (I) <2   2   Total chromium mg/l Cr⁺⁶ (III) <0.05   0.05 Fluorine mg/l F (I) <0.10  1.5 Iron mg/l Fe (I) 0.08 0.3 Magnesium mg/l Mg (I)   1.030 ⁺ 125    Manganese mg/l Mn (I) <0.01   0.10 Mercury mg/l Hg (I)  0.001  0.001 Nitrates mg/l NO₃ (I) 4.54 50   Nitrites mg/l NO₂ (I) 0.04 3   Lead mg/l Pb (I) <0.02   0.05 Total dissolved mg/l (I)   34.310 ⁺ 1,500    solids at 105° C. Selenium mg/l Se (I)  0.001  0.01 Sulfates mg/l SO₄ (I) 2,494 ⁺    500 ⁽²⁾   Free residual chlorine mg/l (III) <0.05  0.2-2.0 in laboratory Nitrate + — (I) <1   1   Nitrite Ratio Organic substances Tetrachloroethene μg/l (*) n.d. 40   Benzene μg/l (*) n.d. 10   Toluene μg/l (*) 0.01 700    Xylenes μg/l (*) n.d. 500    Pesticides D.D.T + D.D.D. + μg/l (*) n.d. 2   D.D.E. 2,4 D μg/l (*) n.d. 30   Lindane μg/l (*) n.d. 2   Methoxychlor μg/l (*) n.d. 20   Pentachlorophenol μg/l (*) n.d. 9   Secondary products of disinfection Monochloramines mg/l (*) <0.1  3   Dibromochloromethane mg/l (*) <0.005 0.1 Dichlorobromomethane mg/l (*) n.d.  0.06 Tribromomethane mg/l (*)  0.037 0.1 Trichloromethane mg/l (*) n.d. 0.2 Trihalomethanes mg/l (I) <1   1   MICROBIOLOGICAL ANALYSIS MEASURED Official EXPRESSED ASSAY VALUE IN THE 2005 NCh PARAMETERS AS METHOD POND 409 Total coliforms MPN/100 ml (V) <2.0 <2.0 Escherichia coli MPN/100 ml (V)-(*) ABSENT ABSENT n.d. Indicates not detected * Official Chilean regulations were used (Chile was the country of the application example), Chilean rule NCh 409 ⁺ Inherent values of sea water.

In this example, it has been demonstrated that it is possible to maintain a water body or volume similar to a large-volume (250,000 m³) artificial sea water pond with a water quality similar to conventional swimming pools and tropical seas, both in its aesthetic characteristics as in its physicochemical and bacteriological properties. The achieved characteristics have not been found in any existing artificial lagoon in the world up to date (see Google Earth) and this can be demonstrated by satellite comparison of the transparency and color of the lagoon to be protected (33″20′59.91″S; 71″39′10.10″W) with the tens of thousands existing in the world, such as golf court and public park lagoons, dams for recreational use, lagoons of real estate and tourist projects, and even dams over 15,000 m³ built with swimming purposes (e.g. Piscina do Ramos in Brazil, Darwin Swimming Pool in Australia, Orthlieb Swimming Pool in Casablanca, Morocco).

We have not found any artificial water body in the world with a volume higher than 15,000 m³ having crystalline water with this quality, except for the structure similar to an artificial lagoon that we want to protect, which has 250,000 m³.

In a Google Earth™ forum (Internet software for satellite photography of the world) people has been searching for two years for the biggest swimming pool in the world that can be seen from the air. The conclusion, when reviewing their results, is that the lagoon of the application example is by far the biggest crystalline water body found.

The biggest known swimming pool in the world that uses traditional filtering and recycling systems is Sunlite Pool of Coney Island, United States, having 11,350 cubic meters of water. In the remaining tens of thousands of large artificial water bodies existing in the world, the water is not filtered or it is only partially filtered. As previously mentioned, the characteristics of the water of these bodies are very different from swimming pools or tropical seas and their uses are limited.

Filtering large water volumes is technically complex and highly costly, and consequently this is a barrier for the scaling-up of crystalline water bodies. The suction device of the present invention removes suspended solids (turbidity) that flocculate together with the polymer in an efficient and economic way, thus replacing filtering.

In addition to the high costs, the traditional filtering system does not solve the cleaning of the bottom of the lagoon.

The technology described in this invention patent, i.e. the replacement of filtering by a suction device and skimmers plus the application of controlled oxidation pulses, which are essential parts of the process, allows breaking the barrier that hinders the construction of crystalline lagoons with unlimited extensions and volumes, thus opening a new field of tourist applications.

The main advantage of the implemented process is evidenced by comparing the regulations for recreational waters and the results obtained in the artificial lagoon of the example. Additionally, the level of transparency obtained in the water is highly important, being the clarity equal or higher than 35 meters, which is a result not found in any water body larger than 15,000 m³ nor in the majority of swimming pools; in fact, the swimming pool regulation demand only 1.4 meters of clarity (see Table 3).

Other advantages of the disclosed process of the present invention are:

-   -   Low maintenance costs.     -   Established regulations for recreational waters with direct         contact are widely fulfilled (see Table 2) and comparable         parameters of the swimming pool and potable water regulations         are also fulfilled (see Tables 3 and 4).     -   The water in the lagoon is always absolutely transparent, with         no turbidity, with the characteristic turquoise color of         swimming pools or tropical seas and with a clean bottom, which         are optimal visual characteristics for the acceptation of the         user public.     -   Use of oxidant, algaecide and disinfectant concentrations up to         100 times lower that those recommended to be applied in         conventional swimming pools; this advantage favors the users and         is more environmentally-friendly.     -   As these water bodies are disconnected from the sea or near         natural lakes, they are not affected by temperature variations         produced by oceanographic currents, ice thawing, etc. but only         by environmental variables (temperature, solar radiation, wind).         In practical terms, in the lagoon of the application example in         summer, temperatures of more that 10° C. higher than those of         the sea are obtained.     -   Flocculation and bottom cleaning by suction together with         skimmers replace the filter system of conventional swimming         pools, thus generating high transparency conditions at a very         low cost. The removal of sediments prevents said sediments to         consume oxidants and generate anoxic zones, and they allow the         bottom membrane to give an attractive tonality to the lagoon's         water.     -   Water bodies can be built with no size limit having optimal         aesthetical, physicochemical and sanitary conditions, which         generates large tourist attraction poles.

In order to make more evident the surprising effect of the process disclosed in the present invention, Table 5 is shown, which illustrate the costs for both cleaning methods in the water body of the application example (250,000 m³).

TABLE 5 Comparison of the traditional filtering method* and the suction device Volume circulated Installation Monthly Specifications through pumps costs operation costs Traditional 120 15 HP Three-phase 2,893 lts/sec US$ 2,686,648⁺ US$ 119,246 filter Aral-C 3000 pumps (Astral code 01206) 60 Praga 3000 filters (Astral code 15781) 714,000 kilograms of sand (Astral code 905000) 60 batteries of 250 mm valves (Astral code 19133) Installation labor Shed of 2,500 m² Total monthly energy required, 24 hours * 30 days * 1343.28 kW/hour (967,164.18 kW/hour) Operators Maintenance Suction Windglider boat   10 lts/sec US$ 25,166 US$ 2,242 device Protected outboard 9.5 HP motor Suction device Suction pump 7.5 HP Hoses, accessories Fuel Flocculant Operator Maintenance *Considering T = 2 (minimal rate for swimming pool filtration) according to regulation NCh 209 ⁺Does not consider the cost of the land for the 2,500 m² shed.

It is important to keep in mind that to obtain the desired final result of “color, transparency and cleanness characteristics similar to swimming pools or tropical seas at low cost”, it is essential to have a water containing structure that have the required elements for water treatment and features that allow obtaining the desired results. The isolated application of the physicochemical process for water treatment would not be possible nor would it produce the desired results. 

What is claimed is:
 1. A process to implement and maintain a large water body, wherein the process comprises: (a) providing a structure with skimmers able to contain a large water body larger than 15,000 m³; (b) feeding the structure of step (a) with inlet water having iron and manganese levels lower than 1.5 ppm and turbidity lower than 5 NTU; (c) measuring water pH, wherein the pH is maintained no lower than 5 and no higher than 9; (d) adding an oxidizing agent to the water body contained in the structure of step (a), to maintain an oxidation-reduction potential (ORP) of at least 600 mV in the water body for at least 4 hours within a 48 hour cycle; (e) adding a flocculating agent to the water body in concentrations within 0.02 and 1 ppm over a time period no greater than 6 days to precipitate impurities in the water to the bottom of the structure of step (a); (f) cleaning the bottom of the structure of step (a) with a movable suction device to remove the precipitated impurities from the bottom of said structure, together with the additional flocculants; and (g) generating a displacement of surface water containing impurities and surface oils by means of injection of inlet water according to step (b), which generates said displacement in such as way to remove said surface water using said skimmers provided in the structure of step (a), which together with step (f) replaces filtration to remove suspended debris from the water body.
 2. The process of claim 1, wherein providing a structure further comprises: providing a bottom and walls made of low permeability materials coated with a non porous material; providing a system for removing impurities and superficial oils using skimmers; providing a feeding pipe system for introduction of fresh water; and providing a feed water intake system.
 3. The process of claim 1, wherein the flocculating agent is a cationic polymer added in concentrations from about 0.02 ppm to about 1 ppm over a time period no greater than 6 days.
 4. The process of claim 1, wherein the flocculating agent is a cationic polymer added at a concentration of 0.05 ppm every 24 hours.
 5. The process of claim 1, wherein bromine salts are added to the water body if the pH is higher than 7.8.
 6. The process of claim 5, wherein the bromine salt is sodium bromide, and wherein the bromide concentration is maintained at values higher than 0.6 ppm.
 7. The process of claim 1, wherein adding an oxidizing agent comprises adding an agent from the group consisting of ozone, sodium persulfate, potassium persulfate, chlorine derivatives, hydrogen peroxide, bromine derivatives, and agents produced by electrochlorination.
 8. The process of claim 1, wherein treating the water to maintain ORP further comprises adding algaecides to the large body of water.
 9. The process of claim 8, wherein the algaecides are selected from the group consisting of quaternary ammonium salts and copper compounds.
 10. The process of claim 9, wherein the copper compounds have copper levels between 1 ppb and 1.5 ppm, depending on temperature and sunlight.
 11. The process of claim 9, wherein the copper compounds are added at copper levels of about 0.3 to about 1.5 ppm for temperatures between 10° C. and 30° C.
 12. The process of claim 1, wherein the inlet water comprises sea water, well water, spring water, or water from other sources.
 13. The process of claim 1, wherein the large water body is for recreational use.
 14. The process of claim 1, comprising adding the oxidizing agent to the water to maintain an ORP of at least 600 mV in the water for about 4 hours within a 24 hour cycle.
 15. The process of claim 1, wherein the large body of water is an outdoor body of water.
 16. The process of claim 1, wherein the oxidizing agent comprises halogen.
 17. The process of claim 16, wherein the halogen is bromine or chlorine. 